Title of article :
Thermodynamic property calculations with the universal mixing rule for EoS/GE models: Results with the Peng–Robinson EoS and a UNIFAC model
Author/Authors :
Voutsas، نويسنده , , Epaminondas and Louli، نويسنده , , Vasiliki and Boukouvalas، نويسنده , , Christos and Magoulas، نويسنده , , Kostis and Tassios، نويسنده , , Dimitrios، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2006
Pages :
13
From page :
216
To page :
228
Abstract :
The universal mixing rule (UMR), which incorporates an activity coefficient model in a cubic equation of state (EoS), and is applicable to all type of system asymmetries up to solvent/polymer ones, has been recently developed in our laboratory [Voutsas et al., Ind. Eng. Chem. Res. 43 (2004) 6238]. The original UNIFAC model with temperature-independent interaction parameters was used in the original publication, which leads, however, to unsatisfactory VLE predictions at high temperatures and poor heats of mixing predictions. In this study the UMR is applied by coupling the translated and modified Peng–Robinson (t-mPR) EoS with an original UNIFAC-type model that utilizes linearly temperature-dependent interaction parameters, eliminating, thus, the aforementioned weaknesses. The performance of the resulting EoS/GE model, referred to as UMR-PRU, utilizing the available UNIFAC interaction parameters, as well as some parameters developed here for gas involving pairs, is evaluated in the prediction and, when necessary, correlation/prediction, of various thermodynamic properties, i.e. VLE, LLE, VLLE, SGE and heats of mixing. The results indicate that the new model represents a unique, simple and reliable tool for thermodynamic property calculations for systems of various degrees of non-ideality and asymmetry, including polymer solutions.
Keywords :
Peng–Robinson , equation of state , UNIFAC , Asymmetric system , Thermodynamic properties , Mixing rule
Journal title :
Fluid Phase Equilibria
Serial Year :
2006
Journal title :
Fluid Phase Equilibria
Record number :
1985757
Link To Document :
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